Classifications

• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
  • C10L1/06—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition

Definitions

• This invention relates to a fuel composition for use in gasoline engines as installed in automobiles and the like, and in particular gasoline engines which correspond to Gasoline No. 1 of the JIS standard (JIS K2202) .
• Various kinds of performance to improve drivability of vehicles and durability of engines are required of fuels for use in the gasoline engines used in automobiles.
• several types of blending component are blended together and prepared whilst taking into account the octane number and distillation characteristics.
• the performance required of a fuel for gasoline engines changes as the social environment changes, so that whenever new demands arise investigations are made of gasoline engine fuel compositions that might apply to them.
• Japanese Laid-open Patent Specification Nos. 2003-277776 and 2006-63264 discloses a fuel additive which has as its main constituent a specified amide compound so as to improve the acceleration response of automobiles.
• the present invention has as its objective to offer a fuel composition for use in gasoline engines which, without any additional conventional fuel additives, has excellent acceleration characteristics at high speeds and excellent fuel consumption.
• the fuel composition of this invention for use in gasoline engines satisfies the conditions: (1) the research octane number is not less than 90; (2) the density is in the range of from 0.740 to 0.760 g/cm 3 ; (3) the distillation temperature at 50 vol% distilled is in the range of from 95 to 105 0 C, the distillation temperature at 90 vol% distilled is in the range of from 160 to 180 0 C, and the distillation end point is not more than 220 0 C; and (4) the content of aromatic hydrocarbons with 9 or more carbon atoms is in the range of from 12 to 20% by volume, and the inda ⁇ e content is in the range of from 1.5 to 3.0% by volume.
• the fuel composition of this invention for use in gasoline engines may also contain in the range of from 4 to 10% by volume of a fraction with a distillation characteristic of from 160 to 230 0 C obtained from fluid catalytic cracking apparatus.
• the aforementioned fraction may also have a content of aromatic hydrocarbons with 9 or more carbon atoms of amount not less than 80% by volume, and an indane content of amount not less than 20% by volume.
• an indane is such as 2, 3-dihydroindene (indane) optionally substituted by at least one functional group which is a hydrocarbon such as an alkyl group, preferably a Ci- to C 4 -alkyl group.
• the number of carbon atoms in an alkyl group bonded to the indane or on the number of groups is not more than 12. If the number of carbon atoms is more than 12, the heavy fractions in the blending component of the gasoline engine fuel obtained will increase and the distillation end point will increase, which is not desirable.
• indane 2,3- dihydroindene (indane), 5-methylindane, 4-methylindane, 1, 2-dimethylindane, 1, 3-dimethylindane, 1,4- dimethylindane, 1, 5-dimethylindane, 1, ⁇ -dimethylindane, 1, 7-dimethylindane, 1, 4, 5-trimethylindane, 1,4,6- trimethylindane, 2, 4, 5-trimethylindane, and 2,4,6- trimethylindane .
• indane 2,3- dihydroindene
• 5-methylindane 4-methylindane
• 2-dimethylindane 1, 3-dimethylindane
• 1,4- dimethylindane 1, 5-dimethylindane
• 1, ⁇ -dimethylindane 1, 7-dimethylindane
• 1, 4, 5-trimethylindane, 1,4,6- trimethylindane 2, 4, 5-trimethylindane, and 2,4,6- trimethylindane .
• the fuel composition of this invention for use in gasoline engines, it is possible, without adding any additional fuel additives, to improve the acceleration characteristics and fuel consumption at high speeds by incorporating in the range of from 12 to 20% by volume of aromatic hydrocarbons with not less than 9 carbons and in the range of from 1.5 to 3.0% by volume of an indane. If the amount of aromatic hydrocarbons with not less than 9 carbon atoms and the amount of indane are less than the aforementioned ranges, the effect of improving the highspeed acceleration performance and fuel consumption will not be achieved, so that it is preferable to increase as far as possible the range at which the necessary conditions can be maintained for the gasoline engine fuel composition. Preferably the amount of aromatic hydrocarbons with not less than 9 carbon atoms is not less than 14% by volume, and the indane content is not less than 2% by volume.
• the fuel compositions of the present invention exhibit improved high-speed acceleration performance and fuel consumption.
• the fuel composition of the present invention for use in gasoline engines can be obtained by incorporating as a blending component in the range of from 4 to 10% by volume of a fraction with a distillation characteristic of in the range of from 160 to 230 0 C obtained from a fluid catalytic cracking apparatus, and in particular a fraction which has a content of aromatic hydrocarbons with 9 or more carbon atoms of amount not less than 80% by volume, and an indane content of amount not less than 20% by volume.
• the blending component which has a distillation characteristic of from 160 to 230 0 C, a content of aromatic hydrocarbons with 9 or more carbon atoms of amount not less than 80% by volume, and an indane content of amount not less than 20% by volume (hereinafter referred to as LLCO) can be obtained by further distillation of light cycle oil corresponding to the kerosene fraction known as middle distillates (distillation characteristic not more than 38O 0 C, hereinafter referred to as LCO) .
• This LLCO has a high research octane number (hereinafter RON) of at least 93, and also contains many indanes.
• LCO hitherto has been used as a blending component for heavy oil "A”, but as it has a low cetane number there have been constraints on its use for diesel- engine heavy oil ⁇ A", so that there is an advantage in relation to effective use of such fractions.
• the proportion of LLCO in the blend can be suitably set in the range of in the range of from 4 to 10% by volume so that the characteristics of the gasoline-engine fuel composition will be within the desired ranges, but given that its distillation characteristics are heavier than for gasoline-engine fuel compositions, in order to satisfy the JIS standard for automobile gasolines (JIS K 2202) , it is necessary in particular to limit the proportion in the blend so that the distillation temperature at 90 vol% distilled (T90) is not more than
• distillation end point is not more than 220 0 C. It is also necessary for there not to be any impact on practical performance as an automotive gasoline engine fuel, and taking this into account the preferred blend proportion is in the range of from 4 to 7% by volume.
• LLCO is obtained by fractionation of ordinary LCO
• the content of aromatic hydrocarbons with not less than 9 carbon atoms is in the amount of from approximately 70 to 90% by volume
• the indane content is in the range of from about 15 to 25% by volume.
• the LLCO cut temperature is made higher, but if the distillation end point exceeds 230 0 C, there will be undesirable problems in that the fuel composition for use in gasoline engines will be made excessively heavy, or the proportion that can be blended in will be restricted.
• the fuel composition of this invention for gasoline engines can be manufactured by mixing in the range of from 4 to 10% by volume of LLCO with ordinary gasoline blending components.
• ordinary gasoline blending components mention may be made of the following.
• Desulphurised light naphtha This is a blending component obtained by desulphurisation of a naphtha obtained from a crude oil atmospheric distillation apparatus, and then by separation into low boiling point fractions by means of distillation.
• Catalytic reformate This is a blending component obtained by desulphurisation of a naphtha obtained from a crude oil atmospheric distillation apparatus and reforming of the remaining heavy fraction separated off by distillation of the aforementioned desulphurised light naphtha, using for example a catalytic reforming method such as Platforming.
• Debenzenated light catalytic reformate This is a blending component obtained by separating the aforementioned catalytic reformate into fractions with a boiling point lower than benzene by means of distillation.
• Catalytic reformates with 7 carbon, 8 carbon, or 9 or more carbon atoms
• Catalytically cracked gasoline This is a blending component obtained by catalytically cracking heavy oil.
• blending components obtained by distillation of the aforementioned catalytically cracked gasoline obtained by catalytic cracking of heavy oil to separate it into fractions with a low boiling point and fractions with a high boiling point.
• the blending component is the result of treating the foul-smelling light sulphur compounds such as mercaptan by sweetening methods such as the Merox method.
• the blending component is the result of removing the sulphur component while ensuring that the reduction in the octane number through olefin hydrogenation is minimised, by using a selective desulphurisation method such as Prime-G+.
• Oxygenates such as alcohols or ethers Mention may be made specifically of, for example, methanol, ethanol and propanol for alcohols.
• ethers mention may be made of MTBE (methyl tertiary butyl ether) and ETBE (ethyl tertiary butyl ether) .
• the types of gasoline blending components used are selected as appropriate to conditions such as the make-up of the apparatus at the refinery. There is no need for all the types of blending component to be mixed in. Consequently, the proportion of any types not used is 0% by volume. Also, when the sulphur content of the LLCO obtained by fractionation of LCO is high, it is possible to carry out, as needed, a desulphurisation treatment such as hydrorefining or adsorption desulphurisation. Examples
• LCO obtained from a catalytic cracking apparatus was further separated in a distillation apparatus into light fractions and heavy fractions.
• a light-fraction LLCO with a distillation characteristic of initial boiling point to 230 0 C was obtained.
• a fuel composition for use in gasoline engines was compounded by blending the LLCO in a commercial regular gasoline (RG) .
• Table 1 shows the characteristics of the LLCO
• Table 2 shows the characteristics of fuel compositions for use in gasoline engines which included the LLCO (Embodiments 1 and 2) .
• Table 2 also shows, in the form of Comparative Example 1, the characteristics of the RG used in the compounding.
• the methods of measurement of the properties shown in Tables 1 and 2 were as follows.
• the TRIAS test method was performed in JCO8 mode (hot start) after sufficient running in warm air.
• the fuel consumption was calculated from the amount of exhaust gases produced during the test by using a carbon balance equation, and the rate of improvement in fuel consumption was expressed as a relative value, taking the commercial PG fuel as a basis.

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• Chemical & Material Sciences (AREA)
• Oil, Petroleum & Natural Gas (AREA)
• Engineering & Computer Science (AREA)
• Chemical Kinetics & Catalysis (AREA)
• General Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Liquid Carbonaceous Fuels (AREA)
• Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
• Lubricants (AREA)

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Citations (4)

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• 2008
  • 2008-12-11 JP JP2008316152A patent/JP5368074B2/ja active Active
• 2009
  • 2009-12-11 CN CN200980154794.4A patent/CN102282239B/zh not_active Expired - Fee Related
  • 2009-12-11 MY MYPI2011002654A patent/MY156372A/en unknown
  • 2009-12-11 RU RU2011128317/04A patent/RU2011128317A/ru not_active Application Discontinuation
  • 2009-12-11 WO PCT/EP2009/066934 patent/WO2010066879A1/en active Application Filing
  • 2009-12-11 BR BRPI0923355-5A patent/BRPI0923355A2/pt not_active IP Right Cessation
  • 2009-12-11 US US13/133,753 patent/US8876920B2/en not_active Expired - Fee Related
  • 2009-12-11 EP EP09775176A patent/EP2367908B1/en not_active Not-in-force
  • 2009-12-11 CA CA2746471A patent/CA2746471A1/en not_active Abandoned

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